Refrigerant composition

ABSTRACT

A refrigerant composition consists essentially of three hydrofluorocarbon components selected from HFC134a, HFC125 and HFC143a and an additive selected from a saturated or unsaturated hydrocarbon or mixture thereof boiling in the range −50° C. and +40° C.

This invention relates to refrigerant compositions. The inventionrelates particularly to refrigerant compositions which have no adverseeffect on stratospheric ozone. The invention also relates tocompositions which are for use both in refrigeration and airconditioning systems designed to use Ozone Depleting Substances (ODS)such as HCFC22 (chlorodifluoromethane) and also for use in newequipment. These refrigerant compositions are compatible with lubricantscommonly found in refrigeration and air conditioning systems and alsothe new synthetic lubricants (eg polyol ester oils).

Although considerable care is taken to prevent leakage of refrigerant tothe atmosphere, on occasions this does occur. In some territories theemission of hydrocarbons is regulated to minimise the generation oftropospheric ozone caused by the effect of sunlight on hydrocarbonsmixed with oxygen. To minimise the contribution of hydrocarbon to theatmosphere by leakage of the blends which are the subject of thisinvention, the hydrocarbon content should be preferably less than 5%more preferably less than 3.5%.

The compositions of this invention may also be used in equipmentdesigned for non ozone depleting substances.

It is well known that chlorofluorocarbons (CFCs) such as CFC12 andCFC502 and hydrochlorofluorocarbons such as HCFC22 while being energyefficient, non flammable and of low toxicity, migrate to thestratosphere where they are broken down by ultra violet light to attackthe ozone layer. It is desirable to replace these Ozone DepletingSubstances by non ozone depleting alternatives such ashydrofluorocarbons (HFCs) which are also non flammable, efficient and oflow toxicity. There are six main HFCs, namely HFC134a, HFC32, HFC125,HFC143a, HFC227ea and HFC152a, which either individually or blended intomixtures can replace CFCs and HCFCs. While HFC134a, HFC227ea and HFC152acan be used to replace ODS directly, HFC32, HFC143a, and HFC125 aregenerally found in blends as replacements for ODS. However, HFCs do nothave adequate solubility in traditional lubricants such as mineral andalkylbenzene oils so that synthetic oxygen containing lubricants havebeen introduced specifically for new equipment. These new lubricants areexpensive and hygroscopic.

Refrigerant blends such as R404A, R507, R410A, R407C and others havebeen commercialised as replacements for CFCs and HCFCs but, becausethese compositions contain only HFC components, they cannot be used withthe traditional lubricants commonly found in use with CFCs and HCFCs. Ifthese blends are to be used to replace CFCs and HCFCs in existingequipment, the major chemical manufacturers recommend that no more than5% of the traditional lubricant in the system be retained so that avirtually complete change of lubricant to a synthetic oxygen containinglubricant or a full retrofit may be required. This is often costly andtechnically unsatisfactory.

Although equipment manufacturers have adapted their units to operatewith HFC blends, the commercially available products have not been foundto be as satisfactory as the CFCs and HCFCs. In particular to ensureadequate oil return, hydrocarbon lubricants, such as mineral oil, havebeen replaced by oxygen containing lubricants, notably polyol esters andpolyalkylene glycols. Unfortunately these materials are liable to absorbatmospheric moisture, especially during maintenance, which cancontribute to excessive corrosion and wear in equipment. This can reducethe reliability of the equipment. It is an object of this invention toprovide HFC/hydrocarbon blends that enable the continued use ofhydrocarbon oils in both existing and new equipment.

In the search for a refrigerant blend that can be readily used toreplace R22 in new & existing equipment, it is especially important thatthe new blend should have an adequate refrigeration capacity. Thecapacity should be at least 90% of that of the fluid it is replacing,more preferably at least 95% of that of the fluid it is replacing andmost preferably equal to or greater than that of the fluid it isreplacing under similar operating conditions. This invention relates torefrigerant compositions which have capacities similar to R22 across therange of applications for air conditioning & refrigeration from high tolow temperatures where R22 is commonly found.

Some refrigerants, such as R407C, have wide temperature glides (>4° C.)in the evaporator and condenser. Equipment manufacturers, based on theirexperience with CFC/HCFC single fluids or azeotropes, preferrefrigerants with low glides. A further object of this invention is toprovide HFC/hydrocarbon blends that can substitute for HCFC 22 and HFCblends such as R407C in order to allow the continued use of hydrocarbonlubricants in equipment and minimising the temperature glides in theheat exchangers by providing azeotropic and near azeotropicformulations.

Various terms have been used in patent literature to describerefrigerant mixtures. The following definitions are taken from Standard34 of the American Society of Heating, Refrigerating & Air ConditioningEngineers (ASHRAE);

Azeotrope: an azeotropic blend is one containing two or morerefrigerants whose equilibrium vapour and liquid phase compositions arethe same at a given pressure. Azeotropic blends exhibit some segregationof components at other conditions. The extent of the segregation dependson the particular azeotrope and the application.

Azeotropic temperature: the temperature at which the liquid and vapourphases of a blend have the same mole fractionation of each component atequilibrium for a specified pressure.

Near azeotrope: a zeotropic blend with a temperature glide sufficientlysmall that it may be disregarded without consequential error in analysisfor a specific application.

Zeotrope: blends comprising multiple components of differentvolatilities that, when used in refrigeration cycles, change volumetriccomposition and saturation temperatures as they evaporate (boil) orcondense at constant pressure.

Temperature glide: the absolute value of the difference between thestarting and ending temperatures of a phase-change process by arefrigerant within a component of a refrigerating system, exclusive ofany subcooling or superheating. This term usually describes condensationor evaporation of a zeotrope.

The present invention relates to near azeotropic and zeotropicrefrigerant compositions, which are non flammable under all conditionsof fractionation as defined under ASHRAE Standard 34, and which can beused to replace ODS in an existing unit without the need to change thelubricant or make any significant change to the system hardware. In newequipment, the refrigerant compositions allow the continued use ofhydrocarbon oils although the unit may be modified to optimise theperformance of the new refrigerant, for example by selecting the mostappropriate lengths of capillary tubes. Where the ingress of moisture orother problems are experienced with oxygen containing oils, the newcompositions allow such oils to be replaced by hydrocarbon oils

It is known in the art that the addition of a small amount ofhydrocarbon to a refrigerant composition containing an HFC or HFCmixtures can result in sufficient hydrocarbon being dissolved in thelubricant to be transported around the system so that lubrication of thecompressor is maintained at all times. It is obvious that the greaterthe hydrocarbon content of the composition the greater the ability ofthe refrigerant to transport the lubricant back to the compressor.However, too high a hydrocarbon content can lead to flammable mixtures.Although flammable refrigerants are acceptable in some applications,this invention relates to non flammable compositions for use inequipment where flammable refrigerants are prohibited. However, it isnot well understood how to achieve non flammable compositions under allconditions including fractionation of the refrigerant compositions whichcan take place during a leak of the refrigerant from the system orduring storage. Flammability in both the liquid and gaseous phases needsto be considered.

Not all HFCs are non flammable as defined under ASHRAE Standard 34.HFC143a and HFC32 have not received a non flammable rating by ASHRAE.This invention relates to compositions of refrigerants which not onlycover blends of non flammable HFCs with hydrocarbons but also blends offlammable HFCs, non flammable HFCs and hydrocarbons in selectedproportions selected so that all such compositions are non flammableduring fractionation while providing similar refrigerating effects andthermodynamic performances as the ODS and HFC blends they replace.

While this invention relates to refrigerant compositions which can beused with traditional lubricants such as mineral and alkylbenzene oils,they are also suitable for use with synthetic oxygen containinglubricants.

In formulating HFC/hydrocarbon blends to replace HCFC 22 in specificapplications, it is sometimes necessary to use one or more lower boilingHFCs, with one or more higher boiling HFCs. In this context preferredlower boiling HFCs are HFC 143a and HFC 125, and the higher boiling HFCis HFC 134a.

To avoid flammability in the blend, or in a fraction generated by aleak, for, example as defined by ASHRAE Standard 34, the total amount ofhydrocarbon should be minimised. At the same time the quantity of thehydrocarbon mixture dissolved in the oil needs to be maximised for goodoil return, especially at those locations in the circuit where the oilis at its most viscous, for example the evaporator. One of the HFCcomponents of this invention, namely HFC143a, has an ASHRAE safetyclassification of A2 which makes the amount of HFC143a used and theselection of the hydrocarbon critical to obtaining a non flammablerating of A1 for the blend. A single higher boiling hydrocarbon, such aspentane or iso-pentane, will concentrate in the liquid phase. This isdemonstrated by leakage tests conducted on a blend of HFC134a, HFC 125and pentane as shown in Example 1.

The National Institute for Standards & Technology (NIST) programmeRefleak—which is widely used to determine the fractionation ofrefrigerant blends under all conditions as required by ASHRAE Standard34—was run for blends comprising HFC134a, HFC143a & R125 with butane andisobutane which produced the results shown in Example 2. Build-up ofbutane in the liquid phase towards the end of the leakage wassignificant at over 60% compared to isobutane at about 15%.

Refleak was run also for blends comprising HFC134a, HFC143a & R125 withisobutane only as shown in Example 3. Build-up of isobutane is shown tobe considerably less than butane in the liquid phase at worst casefractionation. In patent number EP12380 39B1 Roberts teaches away fromthe inclusion of 2-methyl propane (isobutane) in blends containing HFCsdue to flammability concerns at worst case fractionation. Surprisinglyit has been found that the use of isobutane in blends containingHFC134a, HFC143a and HFC125 results in non flammability at worst casefractionation under ASHRAE Standard 34.

This invention enables a flammable HFC such as HFC143a to be used in anon flammable refrigerant blend thereby substantively improving itsperformance, in particular its capacity

According to the present invention a refrigerant composition consistsessentially of:

a hydrofluorocarbon component consisting of a mixture of:

-   -   R134a, R125 and R143a        and an additive selected from a saturated or unsaturated        hydrocarbon or mixture thereof boiling in the range −50° C. and        +40° C.

In preferred embodiments the composition consists of a mixture of thehydrofluorocarbon component and the hydrocarbon component so that nosubstantial amount of any other components or other gases are present.

In a further preferred embodiment the hydrocarbon is present in anamount of 0.1% to 5% and wherein the composition is non-flammable whencompletely in the vapour phase.

In a further preferred embodiment the hydrocarbon is present in anamount of 0.1 to 5% and wherein when the composition is in a containerwhere both vapour and liquid present, neither vapour nor liquid phase isflammable.

The hydrocarbon additions may be selected from the group consisting of2-methylpropane, propane, 2,2-dimethylpropane, n-butane, 2-methylbutane,cyclopentane, hexane, ethane, 2-methylpentane, 3-methylpentane,2,2-dimethylbutane, methylcyclopentane, propene, n-butene, isobutene andmixtures thereof.

In a further embodiment, a refrigerant composition which may findapplication to replace R22 comprises;

-   -   (i) from about 10 to 35 weight percent of HFC134a, preferably 10        to 25 weight percent of HFC134a; and    -   (ii) from about 30 to 79.9 weight percent of HFC125 preferably        46 to 74.7 weight percent of HFC 125; and    -   (iii) from about 10 to 30 weight percent of HFC143a, preferably        15 to 25 weight percent of HFC143a; and    -   (iv) from about 0.1 to 5 weight percent of butane or isobutane        or propane, preferably 0.3 to 4 weight percent of butane or        isobutane or propane.

In a further embodiment, a refrigerant composition which may findapplication to replace R22 comprises:

-   -   (i) from about 10 to 35 weight percent of HFC134a, preferably 10        to 25 weight percent of HFC134a, most preferably 15 to 20 weight        percent of HFC134a; and    -   (ii) from about 25 to 79.8 weight percent of HFC125 preferably        42 to 74.4 weight percent of HFC 125, most preferably 53 to 67.4        weight percent of HFC 125; and    -   (iii) from about 10 to 30 weight percent of HFC143a, preferably        15 to 25 weight percent of HFC143a, and most preferably 17 to 22        weight percent of HFC143a; and    -   (iv) mixtures of butane from about 0.1 to 5 weight percent and        isobutane from about 0.1 to 5 weight percent or mixtures of        butane (0.1 to 5%) and isopentane (0.1 to 5%) or mixtures of        butane (0.1 to 5%) and propane (0.1 to 5%) or mixtures of        isobutane (0.1 to 5%) and propane (0.1 to 5%), preferably 0.3 to        4 weight percent of mixtures of butane (0.3 to 4%) and isobutane        (0.3 to 4%) or mixtures of butane (0.3 to 4%) and isopentane        (0.3 to 4%) or mixtures of butane (0.3 to 4%) and propane (0.3        to 4%) or mixtures of isobutane (0.3 to 4%) and propane (0.3 to        4%), most preferably a mixture of 0.3 to 3 weight percent of        isobutane and 0.3 to 2 weight percent of propane or a mixture of        0.3 to 3 weight percent of butane and 0.3 to 2 weight percent of        propane.

In a further embodiment, a refrigerant composition which may findapplication to replace R22 comprises:

-   -   (i) from about 10 to 35 weight percent of HFC134a, preferably 10        to 25 weight percent of HFC134a; and    -   (ii) from about 20 to 79.7 weight percent of HFC125 preferably        38 to 74.1 weight percent of HFC 125; and    -   (iii) from about 10 to 30 weight percent of HFC143a, preferably        15 to 25 weight percent of HFC143a; and    -   (iv) mixtures of butane from about 0.1 to 5 weight percent and        isobutane from about 0.1 to 5 weight percent and propane from        about 0.1 to 5 weight percent, preferably 0.3 to 4 weight        percent of mixtures of butane (0.3 to 4%) and isobutane (0.3 to        4%) and propane (0.3 to 4%).

A composition which may find application as a replacement for R22consists essentially of:

R134a 16% R125 60% R143a 21% Isobutane 2% Propane 1%

Yet another composition which may find application as a replacement forR22 consists essentially of:

R134a 16% R125 60% R143a 21% Butane 2% Propane 1%

A preferred composition consists essentially of:

R134a 10 to 35% R125 79.9 to 30%   R143a 10 to 30% Butane 0.1 to 5%  

A preferred composition consists essentially of:

R134a 10 to 25% R125 74.7 to 46%   R143a 15 to 25% Butane 0.3 to 4%  

A preferred composition consists essentially of:

R134a 10 to 35% R125 79.9 to 30%   R143a 10 to 30% Isobutane 0.1 to 5%  

A preferred composition consists essentially of:

R134a 10 to 25% R125 74.7 to 46%   R143a 15 to 25% Isobutane 0.3 to 4%  

A preferred composition consists essentially of:

R134a 10 to 35% R125 79.9 to 30%   R143a 10 to 30% Propane 0.1 to 5%  

A preferred composition consists essentially of:

R134a 10 to 25% R125 74.7 to 46%   R143a 15 to 25% Propane 0.3 to 4%  

A preferred composition consists essentially of:

R134a 10 to 35% R125 79.8 to 25%   R143a 10 to 30% Butane 0.1 to 5%  Isobutane 0.1 to 5%  

A preferred composition consists essentially of:

R134a 10 to 25% R125 74.4 to 42%   R143a 15 to 25% Butane 0.3 to 4%  Isobutane 0.3 to 4%  

A preferred composition consists essentially of:

R134a 10 to 35% R125 79.8 to 25%   R143a 10 to 30% Butane 0.1 to 5%  Isopentane 0.1 to 5%  

A preferred composition consists essentially of:

R134a 10 to 25% R125 74.4 to 42%   R143a 15 to 25% Butane 0.3 to 4%  Isopentane 0.3 to 4%  

A preferred composition consists essentially of:

R134a 10 to 35% R125 79.8 to 25%   R143a 10 to 30% Butane 0.1 to 5%  Propane 0.1 to 5%  

A preferred composition consists essentially of:

R134a 10 to 25% R125 74.4 to 42%   R143a 15 to 25% Butane 0.3 to 4%  Propane 0.3 to 4%  

A preferred composition consists essentially of:

R134a 10 to 35% R125 79.8 to 25%   R143a 10 to 30% Isobutane 0.1 to 5%  Propane 0.1 to 5%  

A preferred composition consists essentially of:

R134a 10 to 25% R125 74.4 to 42%   R143a 15 to 25% Isobutane 0.3 to 4%  Propane 0.3 to 4%  

A preferred composition consists essentially of:

R134a 10 to 35% R125 79.7 to 20%   R143a 10 to 30% Butane 0.1 to 5%  Isobutane 0.1 to 5%   Propane 0.1 to 5%  

A preferred composition consists essentially of:

R134a 10 to 25% R125 74.1 to 38%   R143a 15 to 25% Butane 0.3 to 4%  Isobutane 0.3 to 4%   Propane 0.3 to 4%  

A preferred composition consists essentially of:

R134a 15 to 20% R125 67.4 to 53%   R143a 17 to 22% Isobutane 0.3 to 3%  Propane 0.3 to 2%  

A preferred composition consists essentially of:

R134a 15 to 20% R125 67.4 to 53%   R143a 17 to 22% Butane 0.3 to 3%  Propane 0.3 to 2%  

A preferred composition consists essentially of:

R134a 16% R125 60% R143a 21% Isobutane 2% Propane 1%

A preferred composition consists essentially of:

R134a 16% R125 60% R143a 21% Butane 2% Propane 1%

In an embodiment the isobutane is present in an amount of 0.6% to 4% andwherein when the composition is in a container where both vapour andliquid present, neither vapour nor liquid phase is flammable.

In a second, preferred embodiment the hydrocarbon is present in anamount of 0.6 to 3.5%.

In a particularly preferred embodiment, a refrigerant composition whichmay find application to replace R22 comprises:

R134a 15.7%   R125 63% R143a 18% Butane 3.3% 

Yet another preferred composition which may find application as areplacement for R22 consists essentially of:

R134a 15.8%  R125 63% R143a 18% Isobutane 3.2% 

A further preferred refrigerant composition comprises:

R134a 15.9%  R125 63% R143a 18% Isobutane 3.1% 

A preferred refrigerant composition comprises

R134a 16% R125 63% R143a 18% Isobutane 3%

A further preferred refrigerant composition comprises

R134a 16.1%  R125 63% R143a 18% Isobutane 2.9% 

Yet another further preferred refrigerant composition comprises

R134a 16.2%   R125 63% R143a 18% Isobutane 2.8% 

Another further preferred refrigerant composition comprises

R134a 16.3%   R125 63% R143a 18% Isobutane 2.7% 

A further preferred refrigerant composition comprises

R134a 16.4%   R125 63% R143a 18% Isobutane 2.6% 

Yet another preferred refrigerant composition comprises

R134a 16.5%   R125 63% R143a 18% Isobutane 2.5% 

Another preferred refrigerant composition comprises

R134a 16% R125 64% R143a 18% Isobutane  2%

Another preferred refrigerant composition comprises

R134a 15.7%   R125 65% R143a 16% Butane 3.3% 

A further preferred refrigerant composition comprises

R134a 15.8%   R125 65% R143a 16% Isobutane 3.2% 

Yet another further preferred refrigerant composition comprises

R134a 15.9%   R125 65% R143a 16% Isobutane 3.1% 

Yet still another further preferred refrigerant composition comprises

R134a 16% R125 65% R143a 16% Isobutane  3%

A further preferred refrigerant composition comprises

R134a 16.1%   R125 65% R143a 16% Isobutane 2.9% 

Another preferred refrigerant composition comprises

R134a 16.2%   R125 65% R143a 16% Isobutane 2.8% 

Yet another preferred refrigerant composition comprises

R134a 16.3%   R125 65% R143a 16% Isobutane 2.7% 

Yet still another preferred refrigerant composition comprises

R134a 16.4%   R125 65% R143a 16% Isobutane 2.6% 

A further preferred refrigerant composition comprises

R134a 16.5%   R125 65% R143a 16% Isobutane 2.5% 

Another preferred refrigerant composition comprises

R134a 15.7%   R125 67% R143a 14% Butane 3.3% 

Yet another preferred refrigerant composition comprises

R134a 15.8%   R125 67% R143a 14% Isobutane 3.2% 

Yet still another preferred refrigerant composition comprises

R134a 15.9%   R125 67% R143a 14% Isobutane 3.1% 

A further preferred refrigerant composition comprises

R134a 16% R125 67% R143a 14% Isobutane  3%

Another preferred refrigerant composition comprises

R134a 16.1%   R125 67% R143a 14% Isobutane 2.9% 

Yet another preferred refrigerant composition comprises

R134a 16.2%   R125 67% R143a 14% Isobutane 2.8% 

Yet still another preferred refrigerant composition comprises

R134a 16.3%   R125 67% R143a 14% Isobutane 2.7% 

A further preferred refrigerant composition comprises

R134a 16.4%   R125 67% R143a 14% Isobutane 2.6% 

Another preferred refrigerant composition comprises

R134a 16.5%   R125 67% R143a 14% Isobutane 2.5% 

Percentages and other proportions referred to in this specification areby weight unless indicated otherwise and are selected to total 100% fromwithin the ranges disclosed.

The invention is further described by means of examples but not in alimitative sense. The following abbreviations are employed.

-   AF As Formulated blend composition-   WCF Worst Case Formulation: the WCF is defined as the composition    containing the highest (percentage) flammable components within the    manufacturing tolerance range and the lowest amount of non flammable    component.-   WCFF Worst Case Fractionated Formulation: when a blend undergoes a    leak from a package or system, one or more flammable components may    concentrate in the liquid or vapour phases due to fractionation. In    order to evaluate properly the possible flammability risk of a    blend, the worst case formulation (WCF) composition is submitted to    a standard leak test as specified by the ASHRAE 34 protocol. This    leak test can either be experimental or simulated using a computer    program such as NIST's Refleak.

EXAMPLE 1

A blend containing 88% R134a, 10% R125 and 2% pentane was allowed toundergo a vapour phase leak from a cylinder under isothermal conditions.The weight of the cylinder was monitored and the liquid and vapourphases were analysed by gas-liquid chromatography. The first analysiswas made after 2% refrigerant loss. Each subsequent analysis was madeafter 10% of the refrigerant remaining in the cylinder had leaked asshown in Table 1. The experiment was continued until no liquid remainedin the cylinder.

TABLE 1 LIQUID PHASE VAPOUR PHASE R134a R125 Pentane Loss R134a R125Pentane % Wt % Wt % Wt % Wt % Wt % Wt % Wt 88.85 8.55 2.59  2 83.2015.06 1.74 87.31 10.53 2.16 10 86.45 11.33 2.22 90.24 6.95 2.81 10 84.7913.38 1.84 90.65 6.45 2.90 10 85.83 12.23 1.95 90.95 6.08 2.96 10 86.8811.07 2.04 91.58 5.33 3.09 10 87.44 10.50 2.05 91.99 4.71 3.29 10 88.199.67 2.14 91.94 4.73 3.32 10 88.72 9.12 2.16 92.34 4.31 3.34 10 89.738.14 2.21 92.69 3.78 2.53 10 90.17 7.49 2.34 93.05 3.13 3.82 10 90.596.95 2.46 92.97 3.41 3.62 10 91.28 6.43 2.29 93.14 2.94 3.92 10 91.565.98 2.46 93.22 2.78 4.00 10 92.07 5.48 2.45 93.39 2.57 4.03 10 92.485.00 2.52 93.48 2.27 4.25 10 92.76 4.63 2.61 93.52 2.15 4.33 10 93.134.13 2.74 92.30 1.92 4.78 10 93.33 3.98 2.69 93.41 1.75 4.84 10 93.393.56 3.04 93.49 1.59 4.93 10 93.69 3.28 3.03 93.35 1.44 5.21 10 93.833.02 3.15 93.25 1.26 5.49 10 94.12 2.81 3.07 93.33 1.23 5.43 10 94.192.54 3.26 93.08 1.09 5.82 10 95.25 2.40 3.35 92.82 1.03 6.15 10 94.691.44 3.86 92.57 0.88 6.55 10 94.43 2.00 3.57 92.27 0.86 6.87 10 94.241.85 3.91 92.01 0.77 7.22 10 94.44 1.68 3.87 91.39 0.76 7.84 10 10 1.5994.49 90.62 0.58 8.79 10 10 0.87 94.33 89.80 0.54 9.66 10 10 1.31 93.9187.98 0.53 11.49 10 10 1.16 93.65 85.42 0.45 14.13 10 10 1.09 93.6484.26 0.39 15.34 10 10 1.02 93.31 Liquid empty

EXAMPLE 2

A blend with an AF composition of 63% R125, 18% 143a, 15.7% R134a and3.3% isobutane has a WCF composition of 62% R125, 18.9% R143a, 15.7%R134a and 3.4% isobutane. NIST's Refleak programme was used to calculatethe fractionation of this WCF blend for a vapour phase isothermal leaksat 54° C. and −34.4° C. The WCFF compositions under these conditions areshown in Table 2.

TABLE 2 WCFF WCFF 54° C. −34.4° C. AF WCF Liquid Vapour Liquid VapourR125 63 62 52.8 57.6 62 70 R143a 18 18.9 18.7 19 18.9 18.8 R134a 15.715.7 24.7 19.8 15.7 7.4 Isobutane 3.3 3.4 3.83 3.65 3.49 3.73 % wtleaked 82 83

EXAMPLE 3

A blend with an AF composition of 63% R125, 18% 143a, 16% R134a 0.6%butane and 2.4% isobutane has a WCF composition of 62% R125, 18.8%R143a, 16% R134a 0.7% butane and 2.5% isobutane. NIST's Refleakprogramme was used to calculate the fractionation of this WCF blend fora vapour phase isothermal leaks at 54° C. and −34.4° C. The WCFFcompositions under these conditions are shown in Table 3.

TABLE 3 WCFF WCFF 54° C. −34.4° C. AF WCF Liquid Vapour Liquid VapourR125 63 62 52.3 57.3 40.8 55.5 R143a 18 18.8 18.7 18.9 16.4 19.5 R134a16 16 25.1 20.2 40.2 21.7 Butane 0.6 0.7 1.14 0.9 1.1 1.01 Isobutane 2.42.5 2.81 2.67 1.49 2.29 Total hydrocarbon 3 3.2 3.95 3.57 2.59 3.3 % wtleaked 82 83.8

EXAMPLE 4

Blends of R125, R143a, R134a and R600a were evaluated in a typicalhermetic or semi-hermetic air conditioner using NIST's CYCLE D program.

COOLING DUTY DELIVERED 10 kW EVAPORATOR Midpoint evaporating temperature7° C. Superheating 5.0° C. Suction line pressure drop (in saturatedtemperature) 1.5° C. CONDENSER Midpoint fluid condensing temperature45.0° C. Subcooling 5.0° C. Discharge line pressure drop (in saturatedtemperature) 1.5° C. LIQUID LINE/SUCTION LINE HEAT EXCHANGER Efficiency0.3 COMPRESSOR Compressor isentropic efficiency 0.7 Compressorvolumetric efficiency 0.82 Motor efficiency 0.85 PARASITIC POWEREvaporator fan 0.3 kW Condenser fan 0.4 kW Controls 0.1 kW

The results of analysing the performances in an air conditioning unitusing these operating parameters are shown in Table 4, plus R22 forcomparison.

TABLE 4 Refrigerant 1 2 3 4 5 6 7 8 Weight % 60.2 61.8 63 63 63.2 63.564.2 64 125 Weight % 19.8 18.6 18 18 18 18 17 18 143a Weight % 16 1615.7 16 16 16 16 16 134a Weight % 4 3.6 3.3 3 2.8 2.5 2.8 2 600aDischarge 19.53 19.63 19.74 19.77 19.81 19.86 19.83 19.96 pressure (bar)Discharge 76.3 76.2 76.2 76.2 76.2 76.3 76.1 76.3 temperature (° C.) COP(system) 2.42 2.42 2.41 2.41 2.41 2.41 2.41 2.41 Capacity 3035 3046 30583062 3066 3074 3068 3085 (kW/m³) Glide in 1.7 1.7 1.7 1.7 1.7 1.7 1.71.6 evaporator (° C.) Glide in 1.6 1.6 1.6 1.5 1.5 1.5 1.5 1.4 condenser(° C.) Refrigerant 9 10 11 12 13 14 R22 Weight % 64.3 65.7 66.5 66.867.1 69.2 125 Weight % 17.4 16.8 17.1 16.3 18.1 16.2 143a Weight % 15.114.9 15.3 14.1 14 14 134a Weight % 3.2 2.6 1.1 2.8 0.8 0.6 600aDischarge 19.85 20.00 20.24 20.07 20.45 20.53 17.91 pressure (bar)Discharge 76.0 76.0 76.2 75.8 76.2 76.0 104.7 temperature (° C.) COP(system) 2.41 2.41 2.40 2.41 2.40 2.40 2.49 Capacity 3070 3088 3118 30953142 3149 3067 (kW/m³) Glide in 1.6 1.6 1.6 1.6 1.5 1.5 0 evaporator (°C.) Glide in 1.5 1.4 1.3 1.4 1.2 1.2 0 condenser (° C.)

EXAMPLE 5

Blends of R125, R143a, R134a and R600a were evaluated in a typical opencompressor refrigeration unit using NIST's CYCLE D program.

COOLING DUTY DELIVERED 10 kW EVAPORATOR Midpoint evaporating temperature−30° C. Superheating 5.0° C. Suction line pressure drop (in saturatedtemperature) 1.5° C. CONDENSER Midpoint fluid condensing temperature35.0° C. Subcooling 5.0° C. Discharge line pressure drop (in saturatedtemperature) 1.5° C. LIQUID LINE/SUCTION LINE HEAT EXCHANGER Efficiency0.3 COMPRESSOR Compressor isentropic efficiency 0.7 Compressorvolumetric efficiency 0.82 Motor efficiency 0.85 PARASITIC POWEREvaporator fan 0.3 kW Condenser fan 0.4 kW Controls 0.1 kW

The results of analysing the performances in a refrigerator unit usingthese operating parameters are shown in Table 5, plus R22 and R502 forcomparison.

TABLE 5 Refrigerant 1 2 3 4 5 6 7 8 9 Weight % 60.2 61.8 63 63 63.2 63.564 64.2 64.3 125 Weight % 19.8 18.6 18 18 18 18 18 17 17.4 143a Weight %16 16 15.7 16 16 16 16 16 15.1 134a Weight % 4 3.6 3.3 3 2.8 2.5 2 2.83.2 600a Discharge 15.34 15.42 15.51 15.52 15.55 15.60 15.67 15.57 15.59pressure (bar) Discharge 82.9 82.8 82.7 82.8 82.9 82.9 83.0 82.7 82.5temperature (° C.) COP (system) 1.52 1.51 1.51 1.51 1.51 1.51 1.51 1.511.51 Capacity 819 822 825 825 827 828 831 826 829 (kW/m³) Glide in 1.91.9 1.9 1.9 1.9 1.9 1.9 1.9 1.8 evaporator (° C.) Glide in 1.8 1.8 1.71.7 1.7 1.7 1.6 1.7 1.7 condenser (° C.) Refrigerant 10 11 12 13 14 R22R502 Weight % 65.7 66.5 66.8 67.1 69.2 125 Weight % 16.8 17.1 16.3 18.116.2 143a Weight % 14.9 15.3 14.1 14 14 134a Weight % 2.6 1.1 2.8 0.80.6 600a Discharge 15.71 15.89 15.77 16.06 16.12 14.07 15.46 pressure(bar) Discharge 82.5 82.9 82.2 82.8 82.6 132.4 93.5 temperature (° C.)COP (system) 1.51 1.51 1.51 1.50 1.50 1.60 1.55 Capacity 834 840 837 849850 872 907 (kW/m³) Glide in 1.8 1.9 1.8 1.8 1.8 0.0 0.1 evaporator (°C.) Glide in 1.6 1.5 1.6 1.4 1.4 0.0 0.0 condenser (° C.)

1-70. (canceled)
 71. A refrigerant composition consisting essentially ofa refrigerant consisting of: a non-flammable combination ofhydrofluorocarbon and hydrocarbon components formulated as a replacementfor chlorofluorocarbon refrigerant R22, consisting of a mixture of:R134a 10 to 35% R125 79.9 to 30%   R143a 10 to 30% butane 0.1 to 5%  


72. A refrigerant composition as claimed in claim 71 wherein therefrigerant consists of: R134a 10 to 25% R125 74.7 to 46%   R143a 15 to25% butane 0.3 to 4%. 


73. A refrigerant composition as claimed in claim 72 wherein therefrigerant consists of: R134a 15.7%   R125 63% R143a 18% butane 3.3%.


74. A refrigerant composition as claimed in claim 72 wherein therefrigerant consists of: R134a 15.7%   R125 65% R143a 16% butane 3.3%.


75. A refrigerant composition as claimed in claim 72 wherein therefrigerant consists of: R134a 15.7%   R125 67% R143a 14% butane 3.3%.